Effective diffusivity of oxygen in the ash layer of Huadian oil shale semicoke
Yiqun HUANG1, Yiran LI1, Man ZHANG1, Boyu DENG1, Hao KONG1, Junfeng WANG2, Junfu LYU1, Hairui YANG1(), Lingmei WANG3()
1. Key Laboratory for Thermal Science and Power Engineering of the Ministry of Education, State Key Laboratory of Power Systems, Department of Energy and Power Engineering, Tsinghua University, Beijing 100084, China 2. State Key Laboratory of Efficient and Clean Coal-fired Utility Boilers (Harbin Boiler Co., Ltd.), Harbin 150046, China 3. Department of Automation, Shanxi University, Taiyuan 030006, China
Diffusion of oxygen in the ash layer usually dominated the combustion of oil shale semicoke particles due to the high ash content. Thus, effective diffusivity of oxygen in the ash layer was a crucial parameter worthy of careful investigation. In this paper, the effective diffusivity of oxygen in the ash layer of Huadian oil shale semicoke was measured directly using an improved Wicke-Kallenbach diffusion apparatus. The experimental results showed that higher temperature would lead to a higher effective diffusivity and a thicker ash layer had the negative effect. Especially, the effective diffusivity along the direction perpendicular to bedding planes was much lower than that along the direction parallel to bedding planes. In addition, an effective diffusivity model was developed, which could be used to describe the mass transfer of oxygen in the ash layer of oil shale semicoke.
Y A Strizhakova, T V Usova. Current trends in the pyrolysis of oil shale: a review. Solid Fuel Chemistry, 2008, 42(4): 197–201 https://doi.org/10.3103/S0361521908040022
W Kuang, M Lu, I Yeboah, G Qian, X Duan, J Yang, D Chen, X Zhou. A comprehensive kinetics study on non-isothermal pyrolysis of kerogen from green river oil shale. Chemical Engineering Journal, 2019, 377: 120275 https://doi.org/10.1016/j.cej.2018.10.212
4
Y Tian, M Li, D Lai, Z Chen, S Gao, G Xu. Characteristics of oil shale pyrolysis in a two-stage fluidized bed. Chinese Journal of Chemical Engineering, 2018, 26(2): 407–414 https://doi.org/10.1016/j.cjche.2017.02.008
5
X Han, I Kulaots, X Jiang, E Suuberg. Review of oil shale semicoke and its combustion utilization. Fuel, 2014, 126(12): 143–161 https://doi.org/10.1016/j.fuel.2014.02.045
6
Y Yang, X Lu, Q Wang, L Mei, D Song, Y Hong. Experimental study on combustion of low calorific oil shale semicoke in fluidized bed system. Energy & Fuels, 2016, 30(11): 9882–9890 https://doi.org/10.1021/acs.energyfuels.6b01870
7
H Qin, B Sun, Q Wang, M Zhou, H Liu, S Li. Analysis on influence factors of the characteristic of pore structure during combustion of oil shale semi-coke. Proceedings of the CSEE, 2008, 28(35): 14–20 (in Chinese)
8
X Wang, J Wang, J Qian, Y Zhu. Diffusion effects in the ash layer of the oil shale char combustion. Acta Petrolei Sinica (Petroleum Processing Section), 1987, 3(4): 4–11
9
Y Yang, Q Wang, X Lu, J Li, Z Liu. Combustion behaviors and pollutant emission characteristics of low calorific oil shale and its semi-coke in a lab-scale fluidized bed combustor. Applied Energy, 2018, 211: 631–638 https://doi.org/10.1016/j.apenergy.2017.10.071
10
M Mu, X Han, B Chen, X Jiang. Oxidation characteristics of the semicoke from the retorting of oil shale and wheat straw blends in different atmospheres. Oil Shale, 2019, 36(1): 43–61 https://doi.org/10.3176/oil.2019.1.04
11
C R Yörük , T Meriste, S Sener, R Kuusik, A Trikkel. Thermogravimetric analysis and process simulation of oxy-fuel combustion of blended fuels including oil shale, semicoke, and biomass. International Journal of Energy Research, 2018, 42(6): 2213–2224 https://doi.org/10.1002/er.4011
12
P Wang, C Wang, Y Du, Q Feng, Z Wang, W Yao, J Liu, J Zhang, D Che. Experiments and simulation on co-combustion of semi-coke and coal in a full-scale tangentially fired utility boiler. Energy & Fuels, 2019, 33(4): 3012–3027 https://doi.org/10.1021/acs.energyfuels.8b04482
13
J Wang, X Wang. A study of the combustion reaction model of oil shale particles. Acta Petrolei Sinica (Petroleum Processing Section), 1987, 3(3): 1–9
14
Y Huang, M Zhang, J Lyu, H Yang. Modeling study of combustion process of oil shale semicoke in a circulating fluidized bed boiler. Carbon Resources Conversion, 2018, 1(3): 273–278 https://doi.org/10.1016/j.crcon.2018.11.003
15
X Han, X Jiang, J Yan, J Liu. Effects of retorting factors on combustion properties of shale char. 2. porestructure. Energy & Fuels, 2011, 25(1): 97–102 https://doi.org/10.1021/ef101171w
16
J Bai, Q Wang, G Jiao. Study on the pore structure of oil shale during low-temperature pyrolysis. Energy Procedia, 2012, 17(1): 1689–1696 https://doi.org/10.1016/j.egypro.2012.02.299
17
P Tiwari, M Deo, C L Lin, J D Miller. Characterization of oil shale pore structure before and after pyrolysis by using X-ray micro CT. Fuel, 2013, 107(9): 547–554 https://doi.org/10.1016/j.fuel.2013.01.006
18
W Sun, S Chen, M Xu, Y Wei, T Fan, J Guo. The diffusion of molecules inside porous materials with bidisperse pore structures. Chemical Engineering Journal, 2019, 365: 201–219 https://doi.org/10.1016/j.cej.2019.02.039
19
J M Le Blévec, E Barthel, C Briens. Measurement of volatile diffusivity in polymer particles. Chemical Engineering & Processing Process Intensification, 2000, 39(4): 315–322 https://doi.org/10.1016/S0255-2701(99)00091-4
20
Y Zheng, Q Wang, C Yang, T Qiu. Experimental study on mass transport mechanism in poly (styrene-co-divinylbenzene) microspheres with hierarchical pore structure. Chemical Engineering and Processing, 2019, 139: 183–192 https://doi.org/10.1016/j.cep.2019.03.016
O D S Mota, J B L Campos. Combustion of coke with high ash content in fluidised beds. Chemical Engineering Science, 1995, 50(3): 433–439 https://doi.org/10.1016/0009-2509(94)00242-J
23
N M Laurendeau. Heterogeneous kinetics of coal char gasification and combustion. Progress in Energy and Combustion Science, 1978, 4(4): 221–270 https://doi.org/10.1016/0360-1285(78)90008-4
24
J K Sun, R H Hurt. Mechanisms of extinction and near-extinction in pulverized solid fuel combustion. Proceedings of the Combustion Institute, 2000, 28(2): 2205–2213 https://doi.org/10.1016/S0082-0784(00)80630-X
W B Fu, B L Zhang. Experimental determination of the equivalent mass diffusivity for a porous coal-ash particle. Journal of Combustionence & Technology, 1995, 101(3): 371–377 (in Chinese)
28
J H Yan, M J Ni, H T Zhang, K F Cen. Gas diffsuion through the ash layer of coal particle. Journal of Engineering Thermophysics, 1994, 15(3): 341–344 (in Chinese)
29
J Liu, J Yan, X Han, X Jiang. Study on the anisotropy of mass transfer for oxygen in the ash layer of shale char particles. Energy & Fuels, 2010, 24(6): 3488–3497 https://doi.org/10.1021/ef1001919
30
Y Yang, X Lu, Q Wang, D Song, Y Chen, Y Hong. Study on the anisotropy of mass transfer for oxygen in the ash layer of extremely low calorific oil shale semi-coke. Applied Thermal Engineering, 2018, 128: 1494–1501 https://doi.org/10.1016/j.applthermaleng.2017.09.062
31
E Wicke, R Kallenbach. The surface diffusion of carbon dioxide in active carbons. Colloid Journal, 1941, 97(2): 135–151 (in German) https://doi.org/10.1007/BF01502640